We compare the performance of an MTBE synthesis column using two different
hardware configurations: (1) a sieve tray column in which the catalyst part
icles, encased inside wire gauze envelopes, placed along the liquid flow pa
th; (2) a column filled with catalytically active packing of Raschig ring s
hape. The columns simulations are performed using a rigorous nonequilibrium
model. Using the bottoms flow rate of MTBE as continuation parameter it is
shown that the two different hardware configurations exhibit significantly
different bifurcation diagrams. The sensitivity of this bifurcation diagra
m has been studied with varying (a) methanol feed, (b) iso-butene feed, (c)
inert feed and (d) reflux ratio. We show that the cross-flow contacting on
the sieve tray configuration is beneficial to conversion. (C) 2001 Elsevie
r Science B.V. All rights reserved.